FIELD OF THE INVENTION
[0001] The present invention relates to a novel strain of bacteria for use in heavy oil
degradation, a bacteria mixture, a composition for nurturing heavy oil degrading bacteria,
a formulation containing that composition, a method of treating oil components, and
building and civil engineering materials containing a substance treated by that method.
BACKGROUND OF THE INVENTION
[0002] Recent years have seen worsening of ocean pollution throughout the world due to heavy
oil or crude oil leaks from supertanker accidents, submarine oil field development,
etc., and this is one cause of damage to the global environment.
[0003] Conventionally, oils, such as heavy oil and crude oil, leaked into the ocean are
removed through degradation by microorganisms capable of degrading chiefly hydrocarbons
contained in the oils. Specifically, microorganisms which can metabolize and degrade
oil components such as saturated hydrocarbons, aromatic hydrocarbons, etc. are screened
from the natural world, and the screened microorganisms are isolated and grown, after
which a culture solution is prepared for use in degradation of the leaked oil.
[0004] In addition, if the microorganisms are provided with nutrients necessary to grow
during the degrading and removing process, the microbes are able to exercise their
degrading ability to the full. Alternatively, instead of a combination of microorganisms
and nutrients, nutrients alone may be added to the object of treatment (e.g. heavy
oil), so that the oil is removed through degradation by other kinds of microorganisms
having the degrading ability originally present in the vicinity of the object.
[0005] For example, bacteria having a hydrocarbon degrading ability are ordinarily present
at the seashore. Thus, if the hydrocarbon degrading ability the bacteria inherently
possess is activated by providing the bacteria with nutrients, the e.g. heavy oil
can be removed through degradation in an ecologically benign manner, which is advantageous
for environmental protection.
[0006] On the other hand, in order to degrade and remove heavy oil leaked from a supertanker
accident, for example, earth and sand with the heavy oil attached thereto are often
treated without first being separated from the heavy oil. For example, if heavy oil
washed ashore is to be removed through degradation on the seashore, the heavy oil
and the earth and sand are generally not separated from each other before degradation
and removal processing.
[0007] However, when oil, etc. is removed through degradation using microorganisms having
the ability to degrade e.g. hydrocarbons in the above conventional manner, growth
conditions for the microorganisms must be adjusted by providing various kinds of nutrients.
[0008] In other words, in degrading and removing oil components using microorganisms, it
is most effective to use living bacteria in a steady period, which is when they show
their ability to degrade e.g. hydrocarbons to the fullest. However, in order to use
the growing bacteria in the steady period, a culture solution containing expensive
nutrients must be prepared, and setting growth conditions precisely requires tedious
and time-consuming operations. Specifically, a huge quantity of live bacteria are
necessary to remove heavy oil through degradation. Hence, if the required quantity
or cost of the nutrients (nutrient salts) per unit volume of the culture solution
is high, there arises the problem that costs are too high. Further, too much labor
is required to control the growing period.
[0009] Also, in order to use live bacteria in a culture solution in degradation, special
facilities are required in the storage, shipping, etc. of the culture solution, thus
making preparations and operations too complicated.
[0010] On the other hand, using microorganisms to degrade and remove heavy oil from earth
and sand with heavy oil attached thereto without first separating the heavy oil from
the earth and sand also has the problem that further costs are incurred in disposal
of the treated earth and sand, which contain degradation products and residual components
such as asphalt.
SUMMARY OF THE INVENTION
[0011] It is an object of the present invention to provide heavy oil degrading bacteria
and a heavy oil degrading bacteria mixture which are inexpensively prepared, which
simplify degradation and removal operations, and which can be stored and shipped simply,
and to provide a nurturing composition for such bacteria, a method of degrading heavy
oil using such bacteria, a method of treating oil components using such bacteria,
and building and civil engineering materials containing a substance obtained by heavy
oil degradation treatment.
[0012] In order to achieve the above object, the inventors of the present invention conducted
an assiduous study, and completed the present invention when they discovered that
the above object can be achieved by using strains of bacteria collected from seawater
by means of screening, and a mixture thereof.
[0013] Novel strains of bacteria according to the present invention which have a heavy oil
degrading ability and can achieve the above object are FERMBP-7046, a strain belonging
to the genus Acinetobacter; FERMBP-7049, a strain belonging to the genus Acinetobacter;
FERMBP-7047, a strain belonging to the genus Pseudomonas; FERMBP-7048, a strain belonging
to the genus Alcaligenes; FERMBP-7050, a strain belonging to the genus Flavobacterium;
FERMBP-7051, a strain belonging to the genus Flavobacterium; FERMBP-7052, a strain
belonging to the genus Flavobacterium; and FERMBP-7053, a strain belonging to the
genus Moraxella.
[0014] A bacteria mixture according to the present invention which can achieve the above
object is a bacteria mixture including at least one kind of bacteria having a heavy
oil degrading ability selected from the group consisting of: FERMBP-7046, a strain
of Acinetobacter; FERMBP-7049, a strain of Acinetobacter; FERMBP-7047, a strain of
Pseudomonas; FERMBP-7048, a strain of Alcaligenes; FERMBP-7050, a strain of Flavobacterium;
FERMBP-7051, a strain of Flavobacterium; FERMBP-7052, a strain of Flavobacterium;
and FERMBP-7053, a strain of Moraxella.
[0015] The foregoing bacteria or bacteria mixture was discovered when bacteria were isolated
from seawater in order to discover a strain having a hydrocarbon degrading ability
in nutrient-poor conditions as close as possible to those in the natural world. Thus,
the above bacteria or bacteria mixture can be readily grown on inexpensive nutrition
sources and degrade hydrocarbon efficiently. Accordingly, leaked oil components, for
example, can be easily and efficiently removed through degradation at a low cost by
using the foregoing bacteria or bacteria mixture.
[0016] In particular, the above bacteria mixture shows a better ability to degrade oil components
than when each of the foregoing kinds of bacteria is used alone, and for this reason,
heavy oil can be removed through degradation more efficiently by using the above bacteria
mixture.
[0017] In addition, degradation of heavy oil can be further promoted when the bacteria mixture
also includes at least one of FERMBP-7050, a strain of Flavobacterium; FERMBP-7051,
a strain of Flavobacterium; FERMBP-7052, a strain of Flavobacterium; and FERMBP-7053,
a strain of Moraxella.
[0018] Additional objects, features, and strengths of the present invention will be made
clear by the description below. Further, the advantages of the present invention will
be evident from the following explanation in reference to the drawings.
BRIEF DESCRIPTION OF THE DRAWINGS
[0019] Figure 1(a) is an explanatory drawing showing an elution pattern obtained by gas
chromatography analysis, which illustrates degradation and removal of saturated hydrocarbon
components contained in heavy oil by a bacteria mixture according to the present invention,
showing the state before degradation.
[0020] Figure 1(b) is an explanatory drawing showing an elution pattern obtained by gas
chromatography analysis, which illustrates degradation and removal of saturated hydrocarbon
components contained in heavy oil by a bacteria mixture according to the present invention,
showing the state after degradation.
[0021] Figure 2(a) is a graph showing change over time in a quantity of oil remaining when
sand containing 3% by weight of heavy oil attached thereto is treated using a bacteria
mixture or a heavy oil degrading bacteria nurturing composition according to the present
invention.
[0022] Figure 2(b) is a graph showing change over time in a quantity of oil remaining when
sand containing 7% by weight of heavy oil attached thereto is treated using a bacteria
mixture or a heavy oil degrading bacteria nurturing composition according to the present
invention.
[0023] Figure 3(a) is an explanatory drawing showing an elution pattern obtained by gas
chromatography analysis, which illustrates change over time of a saturated hydrocarbon
fraction due to the action of a bacteria mixture and a heavy oil degrading bacteria
nurturing composition according to the present invention on sand with 3% by weight
of heavy oil attached thereto.
[0024] Figure 3(b) is an explanatory drawing showing an elution pattern obtained by gas
chromatography analysis, which illustrates change over time of a saturated hydrocarbon
fraction due to the action of a bacteria mixture and a heavy oil degrading bacteria
nurturing composition according to the present invention on sand with 3% by weight
of heavy oil attached thereto.
[0025] Figure 3(c) is an explanatory drawing showing an elution pattern obtained by gas
chromatography analysis, which illustrates change over time of a saturated hydrocarbon
fraction due to the action of a bacteria mixture and a heavy oil degrading bacteria
nurturing composition according to the present invention on sand with 3% by weight
of heavy oil attached thereto.
[0026] Figure 4(a) is an explanatory drawing showing an elution pattern obtained by gas
chromatography analysis, which illustrates change over time of a saturated hydrocarbon
fraction due to the action of a heavy oil degrading bacteria nurturing composition
according to the present invention on sand with 3% by weight of heavy oil attached
thereto.
[0027] Figure 4(b) is an explanatory drawing showing an elution pattern obtained by gas
chromatography analysis, which illustrates change over time of a saturated hydrocarbon
fraction due to the action of a heavy oil degrading bacteria nurturing composition
according to the present invention on sand with 3% by weight of heavy oil attached
thereto.
[0028] Figure 4(c) is an explanatory drawing showing an elution pattern obtained by gas
chromatography analysis, which illustrates change over time of a saturated hydrocarbon
fraction due to the action of a heavy oil degrading bacteria nurturing composition
according to the present invention on sand with 3% by weight of heavy oil attached
thereto.
[0029] Figure 5(a) is a graph explaining change in composition of heavy oil components due
to treatment of sand with 3% by weight of heavy oil attached thereto using a bacteria
mixture or a heavy oil degrading bacteria nurturing composition according to the present
invention.
[0030] Figure 5(b) is a graph explaining change in composition of heavy oil components due
to treatment of sand with 7% by weight of heavy oil attached thereto using a bacteria
mixture or a heavy oil degrading bacteria nurturing composition according to the present
invention.
DESCRIPTION OF THE EMBODIMENTS
[0031] The following will explain an embodiment of the present invention with reference
to the drawings.
[FIRST EMBODIMENT]
[0032] Each of the bacteria strains according to the present invention, i.e. FERMBP-7046,
a strain belonging to the genus Acinetobacter; FERMBP-7049, a strain belonging to
the genus Acinetobacter; FERMBP-7047, a strain belonging to the genus Pseudomonas;
and FERMBP-7048, a strain belonging to the genus Alcaligenes, is a novel strain collected
from the natural world by means of screening, and each was isolated as a useful microorganism
having the ability to degrade hydrocarbons, for example to degrade oil components,
such as heavy oil.
[0033] In the present invention, "ability to degrade heavy oil" means not only an ability
to degrade relatively high-molecule hydrocarbons contained in the heavy oil, but also
an ability to degrade relatively low-molecule hydrocarbons resulting from degradation
of the foregoing relatively high-molecule hydrocarbons.
[0034] In addition, a bacteria mixture including at least one bacteria strain selected from
the group consisting of the foregoing four strains, and this bacteria mixture further
including a bacteria group consisting of a strain belonging to the genus Flavobacterium
and/or a strain belonging to the genus Acinetobacter shows even better hydrocarbon
degrading ability than the above four kinds of strains when each is added separately
to the object of treatment.
[0035] The following will explain the process by which the bacteria of the present invention
were isolated.
[0036] The Acinetobacter strain FERMBP-7046 (TFBOL-1), the Acinetobacter strain FERMBP-7049
(TFBOL-7), the Pseudomonas strain FERMBP-7047 (TFBOL-2), and the Alcaligenes strain
FERMBP-7048 (TFBOL-3) of the present invention are bacteria which were isolated from
natural seawater.
[0037] The first screening was carried out in the following manner.
[0038] A culture medium having the composition set forth in Table 1 below was used as an
isolating culture medium for isolating bacteria from a total of 50 samples of seawater,
water, and sediment collected from harbors, offshore waters, and rivers throughout
Japan. This composition was used because the carbon source used was fluid paraffin
(nacalai tesque K.K.), in order to isolate strains having a hydrocarbon degrading
ability under nutrient-poor conditions as close as possible to those in the natural
world. Here, fluid paraffin is defined as a saturated hydrocarbon mixture having 15-30
carbon atoms.
(TABLE 1)
| FLUID PARAFFIN (LIGHT) |
10.0g |
| AMMONIUM CHLORIDE |
100mg |
| POTASSIUM PHOSPHATE MONOBASIC |
10mg |
| DISTILLED WATER (OR SEAWATER) |
1000ml |
| pH |
6.5-7.0 |
[0039] Each of the foregoing samples of seawater, etc. was isolated by means of filtration
(pore diameter: 0.45
µm), and 1 ml (in case of liquid filtrate) or 1 g (in case of solid filtrate) of the
sample was added to a 500-ml shaking flask with 100ml of the foregoing isolating culture
medium which had been sterilized by wet heat sterilization (121°C; 20 min.)
[0040] The mixture of the sample and isolating culture medium was cultured by shaking (120
strokes/min.; 5cm; 30°C) for 7-10 days, and an accumulation culture was conducted
by planting 1 ml of the culture solution to a new isolating culture medium a total
of four times in succession. The microorganisms present in the fourth accumulative
culture solution obtained thereby were mixed saturated hydrocarbon degrading bacteria.
[0041] Then the second screening was carried out in the following manner. The foregoing
accumulative culture solution containing the mixed bacteria was mixed with the isolating
culture medium at a volume ratio of 1:1, and the resulting mixture was cultured by
shaking (120 strokes/min.; 5cm; 30°C), and then visually observed. A culture solution
in which the emulsification and dispersion rates of the fluid paraffin were observed
to be at or above their respective predetermined rates, and having the lowest observed
n-hexane extract fraction quantity after seven days of culturing, was obtained as
an excellent mixed strain. The following will explain in detail the second screening.
[0042] First, the mixed saturated hydrocarbon degrading bacteria obtained by the foregoing
accumulation culture were cultured by shaking (120 strokes/min.; 5cm; 25°C) for four
days in a preparatory culture medium having the composition set forth in Table 2 below,
yielding a preparatory culture solution, from which bacteria were collected by centrifuge
separation (3500 rpm; 20 min.). Then the collected bacteria were washed twice with
the preparatory culture medium, yielding lml of a bacteria suspension. Next, 1ml of
the foregoing bacteria suspension (bacteria count: 10
9/ml) was inoculated into a 500-ml shaking flask containing 100ml of a basic salt culture
medium having the composition set forth in Table 3 below, and cultured by shaking
(120 strokes/min.; 5cm; 30°C).
(TABLE 2)
| FLUID PARAFFIN (LIGHT) |
10.0g |
| MAGNESIUM SULFATE HEPTAHYDRATE |
0.2g |
| CALCIUM CHLORIDE |
0.02g |
| POTASSIUM PHOSPHATE MONOBASIC |
1.0g |
| POTASSIUM PHOSPHATE DIBASIC |
1.0g |
| AMMONIUM NITRATE |
1.0g |
| IRON (III) CHLORIDE HEXAHYDRATE |
0.05g |
| SODIUM CHLORIDE |
20.0g |
| DISTILLED WATER |
1000ml |
| pH |
6.5-7.0 |
(TABLE 3)
| FLUID PARAFFIN (LIGHT) |
10.0g |
| AMMONIUM NITRATE |
0.1g |
| POTASSIUM PHOSPHATE DIBASIC |
1.0g |
| MAGNESIUM SULFATE HEPTAHYDRATE |
0.2g |
| IRON (III) CHLORIDE HEXAHYDRATE |
0.05g |
| CALCIUM CHLORIDE |
0.02g |
| YEAST EXTRACT |
0.01g |
| SODIUM CHLORIDE |
20.0g |
| DISTILLED WATER |
1000 ml |
| pH |
6.5-7.0 |
[0043] A sample was collected from the foregoing culture solution, and absorbance of 610nm
light was measured using a spectrophotometer (Shimadzu Corporation model UV-1200),
yielding mixed bacteria which were in the steady period after culturing for seven
days. The bacteria count of the resulting mixed bacteria was computed by measuring
absorbance of 610nm light by the bacteria suspension using the spectrophotometer.
[0044] The quantity of an n-hexane extract fraction, that is, the quantity of saturated
hydrocarbons deriving from the fluid paraffin remaining in the culture solution, was
measured in the following manner.
[0045] First, the culture solution was extracted twice by using 100 ml of n-hexane, and
100 ml of the extracted culture solution was passed through a column of sodium sulfate
anhydride, whereby the culture solution was dehydrated and the bacteria was removed
therefrom and concentrated. The resulting product was then purified by active alumina
chromatography (active alumina: 200 mesh, 60 ml, Wako Pure Chemical Industries, Ltd.;
glass column: Pyrex™ Glass, 20mm×600mm, flow rate: 20ml/h), thereby removing metabolites
such as fatty acid. Then the resulting product was dried (60°C in the presence of
air flow) until it reached a constant weight. Here, the weight of the dried product
was treated as the quantity of an n-hexane extract fraction, i.e., the quantity of
residual saturated hydrocarbon.
[0046] The quantity of the n-hexane extract fraction was determined by means of gas chromatography.
Analysis conditions for the gas chromatography were as follows:
| Column |
SUPPORT PETROCOL B COLUMN (SUPELCO) |
| Oven temp. |
50°C to 350°C, 10°C/min |
| Injector temp. |
300°C |
| Detection temp. |
360°C |
| Detector |
FID |
| Carrier gas |
helium |
[0047] Further, degree of emulsification of the fluid paraffin into the culture solution
was measured by removing the bacteria from the culture solution by means of centrifuge
separation (3500 rpm; 20 min.), and then measuring the absorbance of the supernatant
of light having a wavelength of 610nm.
[0048] From five kinds of samples obtained through the foregoing first and second screenings,
the mixed bacteria having the fastest fluid paraffin emulsification rate and the smallest
n-hexane extract fraction quantity after culturing for seven days was obtained. This
was a saturated hydrocarbon degrading bacteria group obtained from seawater, and included
the FERMBP-7046 Acinetobacter strain (TFBOL-1), the FERMBP-7049 Acinetobacter strain
(TFBOL-7), the FERMBP-7047 Pseudomonas strain (TFBOL-2), and the FERMBP-7048 Alcaligenes
strain (TFBOL-3).
[0049] Next, each strain was isolated from the saturated hydrocarbon degrading bacteria
group obtained in the above manner. Here, the isolating culture mediums used were
a hydrocarbon plate culture medium and a common agar culture medium, obtained by the
method proposed by Baruah et al. (Toru KODAMA,
Methods of Separating Microorganisms, R & D Planning Co.). The hydrocarbon plate culture medium was obtained by the following
steps:
putting the fluid paraffin in a powder form in advance by letting the fluid paraffin
be absorbed into silica gel;
making a slurry of the paraffin powder by suspension in a small quantity of water;
and
mixing the slurry homogeneously with an agar culture medium prepared by adding 2%
by weight of agar to the basic salt culture medium shown in Table 2 above.
[0050] A culture solution including the saturation hydrocarbon degrading bacteria group
was applied onto the foregoing isolating culture medium by spraying, and cultured
for 48 hours at 27°C. Then, expressed colonies were collected and cultured for two
to three days at 37°C, whereby four strains, that is, bacteria TFBOL-1, TFBOL-2, TFBOL-3,
and TFBOL-7, were obtained as the strains according to the present invention.
[0051] Subsequently, each isolated strain according to the present invention was identified
in accordance with the method disclosed in
Bergey's Manual of Determinative Bacteriology, 9th Edition.
[0052] In identifying the bacteria TFBOL-1 through TFBOL-8, the genus and species were found
by conducting physiological experiments for each of (1) morphological characteristics
including configuration of nutrient cells, polymorphism of the cell, maneuverability,
and presence of spores; and (2) physiological characteristics including Gram's staining,
catalase reaction, oxidase reaction, fermentation (generation of acid or gas from
sugars) as well as development under anaerobic and aerobic conditions. The results
are set forth in Table 4 below.
(TABLE 4)
| CHARACTERISTICS |
TFBOL |
| |
1 |
2 |
3 |
4 |
5 |
6 |
7 |
8 |
| GRAM'S STAINING |
- |
- |
- |
- |
- |
- |
- |
- |
| CELL POLYMORPHISM |
R |
R |
R |
R |
R |
R |
R |
R |
| MANEUVERABILITY |
- |
+ |
+ |
- |
- |
- |
- |
- |
| DEVELOPMENT UNDER: |
|
|
|
|
|
|
|
|
| AEROBIC CONDITIONS |
+ |
+ |
+ |
+ |
+ |
+ |
+ |
+ |
| ANAEROBIC CONDITIONS |
- |
+ |
- |
- |
- |
- |
- |
- |
| CATALASE REACTION |
+ |
+ |
+ |
+ |
+ |
+ |
+ |
+ |
| OXIDASE REACTION |
- |
+ |
+ |
+ |
+ |
+ |
- |
+ |
| ACID GENERATION FROM SUGARS |
+ |
+ |
- |
+ |
+ |
+ |
+ |
- |
| OF TEST |
O |
O |
- |
O |
O |
O |
O |
- |
| (+: POSITIVE; -: NEGATIVE; S: SPHERICAL; R: ROD; O: OXIDATION) |
[0053] Table 4 shows that the strains TFBOL-1 and TFBOL-7 were Gram negative short bacilli
having no maneuverability, which did not grow under anaerobic conditions, and which
showed positive in the catalase reaction, negative in the oxidase reaction, and O
(oxidation) in the fermentation test (Oxidation-Fermentation Test). Based on these
results, the TFBOL-1 TFBOL-7 strains were identified as bacteria of the genus Acinetobacter.
[0054] The strains TFBOL-1 and TFBOL-7 were domestically deposited with the National Institute
of Bioscience and Human Technology of the Agency of Industrial Science and Technology
(AIST) (1-3 Higashi 1-chome, Tsukuba-shi, Ibaraki-ken, Japan 305-8566) on February
24, 1999, and were assigned Accession Nos. FERMP-17233 and FERMP-17236, respectively.
[0055] The strains TFBOL-1 and TFBOL-7 were later internationally deposited with the National
Institute of Bioscience and Human Technology of AIST on February 23, 2000 and were
assigned Accession Nos. FERMBP-7046 and FERMBP-7049, respectively.
[0056] The strain TFBOL-2 was a Gram negative short bacillus having maneuverability, which
developed under anaerobic conditions and showed positive in both the catalase reaction
and oxidase reaction, and O in the OF test. Based on these results, the TFBOL-2 strain
was identified as bacteria of the genus Pseudomonas.
[0057] The strain TFBOL-2 was domestically deposited with the National Institute of Bioscience
and Human Technology of AIST on February 24, 1999 and assigned Accession No. FERMP-17234.
[0058] Later, the TFBOL-2 strain was internationally deposited with the National Institute
of Bioscience and Human Technology of AIST on February 23, 2000 and assigned Depository
No. FERMBP-7047.
[0059] The strain TFBOL-3 was a Gram negative short bacillus having maneuverability, which
did not develop under anaerobic conditions, showed positive in both the catalase reaction
and oxidase reaction, and did not generate acid from glucose. Based on these results,
the TFBOL-3 strain was identified as bacteria of the genus Alcaligenes.
[0060] The strain TFBOL-3 was domestically deposited with the National Institute of Bioscience
and Human Technology of AIST on February 24, 1999 and assigned Accession No. FERMP-17235.
[0061] Later, the strain TFBOL-3 was internationally deposited with the National Institute
of Bioscience and Human Technology of AIST on February 23, 2000 and assigned Accession
No. FERMBP-7048.
[0062] The strains TFBOL-4, TFBOL-5, and TFBOL-6 were Gram negative short bacilli having
no maneuverability, which did not develop under anaerobic conditions, and showed positive
both in the catalase reaction and oxidase reaction, and O in the OF test. Based on
these results, the strains TFBOL-4, -5, and -6 were identified as bacteria of the
genus Flavobacterium.
[0063] The strains TFBOL-4, TFBOL-5, and TFBOL-6 were internationally deposited with the
National Institute of Bioscience and Human Technology of AIST on February 23, 2000
and assigned Accession Nos. FERMBP-7050, FERMBP-7051, and FERMBP-7052, respectively.
[0064] The strain TFBOL-8 was a Gram negative short bacillus having no maneuverability,
which did not develop under anaerobic conditions, showed positive in both the catalase
reaction and oxidase reaction, and did not produce acid from glucose. Based on these
results, the TFBOL-8 strain was identified as bacteria of the genus Moraxella.
[0065] The strain TFBOL-8 was internationally deposited with the National Institute of Bioscience
and Human Technology of AIST on February 23, 2000 and assigned Accession No. FERMBP-7053.
[0066] Of the above bacteria according to the present invention, the FERMBP-7046 strain
of Acinetobacter (TFBOL-1), the FERMBP-7047 strain of Pseudomonas (TFBOL-2), the FERMBP-7048
strain of Alcaligenes (TFBOL-3), and the FERMBP-7049 strain of Acinetobacter (TFBOL-7)
show activity in degrading saturated hydrocarbons present in oil components such as
heavy oil when used individually, and also when used as necessary in a bacteria mixture.
[0067] Also, of the above bacteria, the FERMBP-7050 strain of Flavobacterium (TFBOL-4),
the FERMBP-7051 strain of Flavobacterium (TFBOL-5), the FERMBP-7052 strain of Flavobacterium
(TFBOL-6), and the FERMBP-7053 strain of Moraxella (TFBOL-8) show excellent degradation
activity when mixed with at least one of the TFBOL-1, TFBOL-2, TFBOL-3, and TFBOL-7
and used as the bacteria mixture.
[0068] In particular, in decomposing saturated hydrocarbons present in oil components such
as heavy oil, it is especially preferable to use a bacteria mixture containing all
of TFBOL-4, -5, -6, and -8 and TFBOL-1,-2, -3, and -7.
[0069] Herein, "bacteria mixture" means a mixture including at least two different kinds
of bacteria.
[0070] In the bacteria mixture according to the present invention, the Flavobacterium strain
TFBOL-4, the Flavobacterium strain TFBOL-5, the Flavobacterium strain TFBOL-6, and
the Moraxella strain TFBOL-8, either individually or in combination, may be included
in the foregoing bacteria mixture as necessary.
[0071] Each of the strains TFBOL-4, TFBOL-5, TFBOL-6, and TFBOL-8 has poor activity in degrading
saturation hydrocarbon when used alone, but it was found that when these strains are
added to the bacteria TFBOL-1, -2, -3, or -7 or to the bacteria mixture according
to the present invention, the bacteria or bacteria mixture shows better activity in
degrading saturated hydrocarbons, for the same bacteria count, than when these strains
are not added.
[0072] The mechanism of why degrading activity is improved by adding these strains is not
clear. However, it is presumed that, while the bacteria or bacteria mixture of the
present invention degrades saturated hydrocarbons, the TFBOL-4, -5, -6, and -8 strains
degrade other oil components, such as aromatic hydrocarbons.
[0073] A heavy oil degrading bacteria nurturing composition of the present invention essentially
includes 40 to 90 wt% of ammonium nitrate, 1 to 50 wt% of potassium phosphate dibasic,
2 to 50 wt% of magnesium sulfate, 1 to 20 wt% of iron (III) chloride, 0.2 to 15 wt%
of calcium chloride, and 0.1 to 10 wt% of yeast extract as effective components.
[0074] The concentration of ammonium nitrate is preferably in a range from 60 through 80
wt%, and more preferably in a range from 70 through 75 wt%.
[0075] The concentration of potassium phosphate dibasic is preferably in a range from 2
through 25 wt%, and more preferably in a range from 5 through 10 wt%.
[0076] The concentration of magnesium nitrate is preferably in a range from 4 through 25
wt%, and more preferably in a range from 10 through 20 wt%.
[0077] The concentration of iron (III) chloride is preferably in a range from 2 through
10 wt%, and more preferably in a range from 3 through 5 wt%.
[0078] The concentration of calcium chloride is preferably in a range from 0.6 through 5
wt% and more preferably in a range from 1 through 3 wt%.
[0079] The concentration of yeast extract is preferably in a range from 0.2 through 3 wt%
and more preferably in a range from 0.5 through 1 wt%.
[0080] The foregoing heavy oil degrading bacteria nurturing composition is used suitably
as a component of a nutrient salt culture medium to culture and store microorganisms
including bacteria, actinomyces, yeast, etc. having the ability to degrade hydrocarbons
such as heavy oil. This heavy oil degrading bacteria nurturing composition is particularly
suitable when included in a nutrient salt culture medium used to culture and store
the bacteria and bacteria mixture according to the present invention.
[0081] For example, when the bacteria and bacteria mixture of the present invention are
to be used as heavy oil degrading bacteria, the heavy oil degrading bacteria nurturing
composition is made into an aqueous solution by dilution with 500 to 2000 times its
weight of water, seawater, etc. Then, the bacteria or bacteria mixture are cultured
in or added to the aqueous solution in a quantity and at a concentration which allows
expression of heavy oil degrading activity, and by allowing the same to act on an
object of treatment, such as heavy oil, the heavy oil can be removed through degradation.
The concentration of the heavy oil degrading bacteria nurturing composition in the
aqueous solution is not especially limited. However, as was mentioned, it is preferable
to dissolve or dilute the same with 500 to 2000 times its weight of water or seawater.
[0082] It is also possible to remove heavy oil through degradation by adding the heavy oil
degrading bacteria nurturing composition alone or in the form of the aqueous solution,
without adding the bacteria or bacteria mixture, to earth and sand with e.g. heavy
oil attached thereto. In other words, the degradation of hydrocarbons contained in
the heavy oil can be promoted by growing and activating microorganisms present in
the earth and sand using the heavy oil degrading bacteria nurturing composition.
[0083] As noted above, the essential components function sufficiently even in small amounts.
Also, the heavy oil itself can be used as a carbon source for growing the heavy oil
degrading bacteria, thus making some other carbon source, such as peptone, unnecessary.
Thus, the heavy oil degrading bacteria nurturing composition can be prepared at a
lower cost than with the conventional method, and is particularly useful as a culture
medium to grow and store a large volume of heavy degrading bacteria.
[0084] The nutrient salt culture medium including the heavy oil degrading bacteria nurturing
composition may additionally include inorganic compounds such as salts, or organic
compounds such as fluid paraffin, where necessary.
[0085] When an aqueous solution of the dissolved or diluted heavy oil degrading bacteria
nurturing composition is used, pH of the aqueous solution can be set arbitrarily depending
on the kind of microorganisms used. However, pH is preferably in a range from 5.0
through 8.0, more preferably in a range from 6.0 through 7.5, and most preferably
in a range from 6.5 through 7.0.
[0086] Examples of objects of treatment by the bacteria, bacteria mixture, heavy oil degrading
bacteria nurturing composition, or formulation according to the present invention
include: saturated hydrocarbons having 17-40 carbon atoms; aromatic hydrocarbons such
as benzene, toluene, and naphthalene; heavy oil including the above saturated hydrocarbons
or aromatic hydrocarbons and other kinds of oil components; etc.
[0087] A formulation according to the present invention is a formulation which contains
the heavy oil degrading bacteria nurturing composition alone, or in a combination
with the bacteria or bacteria mixture, other kinds of microorganisms having the heavy
oil degrading ability, water, etc. The form of the formulation is not especially limited,
and it can be in the form of pellets, sheets, balls, etc.
[0088] Specifically, starch, cellose, zeolite, vermiculite, sponge, etc. can be impregnated
with, for example, an aqueous solution of the heavy oil degrading bacteria nurturing
composition and the bacteria or bacteria mixture, and formed into pellets or sheets,
or formed into solid form as balls, or sealed in a capsule having biodegradability.
[0089] The present formulation is used to degrade and remove heavy oil by spreading (scattering,
etc.) these pellets or balls of the formulation over the beach where the heavy oil
was washed ashore, and leaving for a time sufficient for degradation of the heavy
oil to proceed. By using pellets, balls, or capsules of the formulation, the heavy
oil degrading bacteria nurturing composition and the bacteria or bacteria mixture
solidified in the formulation gradually washed into the object of treatment. In this
manner, the degrading action to the e.g. heavy oil can be maintained for a considerably
long time.
[0090] By using the formulation of the present invention as has been discussed, heavy oil
can be removed through degradation efficiently over a wide area by quite simple operations.
[0091] The formulation may be scattered manually, or using a machine such as a sower where
necessary.
[0092] The form of the object of treatment, from which oil components such as heavy oil
are to be removed through degradation by using the bacteria, bacteria mixture, heavy
oil degrading bacteria nurturing composition, or formulation according to the present
invention is not especially limited. Examples of the object of treatment include heavy
oil leaked to the ocean surface due to a shipwreck, earth and sand with heavy oil
attached thereto, structures such as a vessel with heavy oil attached thereto, a reef
with heavy oil attached thereto, etc.
[0093] In a method of treating oil components according to the present invention, at least
one of the bacteria, bacteria mixture, heavy oil degrading bacteria nurturing composition,
and formulation is added directly to the object having the oil components such as
heavy oil, and left for a sufficiently long time for the degradation of the heavy
oil to proceed. Alternatively, an object of treatment such as earth or sand can be
treated by placing the earth or sand with e.g. heavy oil attached thereto in a column,
and adding a solution containing the bacteria, bacteria mixture, and heavy oil degrading
bacteria nurturing composition from the top of the column.
[0094] The temperature of the foregoing treatment is preferably in a range from 15°C through
45°C, more preferably in a range from 20°C through 35°C, and most preferably in a
range from 22°C through 28°C.
[0095] More specifically, examples of the present method of treating oil components include:
a method in which a culture solution including the bacteria or bacteria mixture grown
to the steady period is directly added to the object; a method in which only a solution
including the heavy oil degrading bacteria nurturing composition is directly added
to the object; a method in which the heavy oil degrading bacteria nurturing composition
additionally including the bacteria or bacteria mixture is directly added to the object;
and a method in which the foregoing solution is added to a container filled with the
object, such as earth and sand.
[0096] When removing oil components such as heavy oil through degradation, the number of
bacteria in the bacteria or bacteria mixture according to the present invention is
not especially limited. However, a preferable range is from 1×10
6 to 1×10
9 per 1g of the object with heavy oil attached thereto.
[SECOND EMBODIMENT]
[0097] As discussed in the first embodiment above, earth and sand with oil components such
as heavy oil attached thereto can be treated using at least one of the bacteria strain,
bacteria mixture, heavy oil degrading bacteria nurturing composition, and formulation
containing that composition, according to the present invention. This treatment yields
treated substance from which the heavy oil has been degraded, leaving recycled sand.
[0098] The present embodiment investigates whether it is possible to use the sand obtained
as treated substance by the foregoing treatment (hereinafter referred to as "recycled
sand") as an aggregate or supplementary material in asphalt concrete for road paving
or in cement mortar, i.e., whether the recycled sand can be practically used as a
building and civil engineering material. The specific investigations made will be
discussed in the Examples below.
[0099] As a result, with respect to use of the recycled sand as asphalt concrete for road
paving, the foregoing investigations yielded the following results.
[0100] Specifically, when a recycled sand A, obtained by treating sand with 7% by weight
of heavy oil attached thereto using a nutrient salt culture medium containing the
foregoing heavy oil degrading bacteria nurturing composition and bacteria mixture
for 56 days, and a recycled sand B, obtained by treating sand with 7% by weight of
heavy oil attached thereto using only the nutrient salt culture medium containing
the foregoing heavy oil degrading bacteria nurturing composition, were each dried
in a bulk drier and added to an aggregate for asphalt concrete in the amount of 15%
of the total aggregate, it was found that the aggregates obtained thereby easily met
standards for asphalt concrete for road paving.
[0101] Incidentally, the results of the Examples to be discussed below indicate that the
foregoing aggregates met standards for asphalt concrete for road paving with a margin
to spare. Accordingly, an aggregate containing the recycled sand A or the recycled
sand B in the amount of 20% to 30% of the total aggregate can also be expected to
be applicable in asphalt concrete for road paving.
[0102] When one of the foregoing aggregates is used in asphalt concrete for road paving,
it is generally heated to no less than 160°C during application. For this reason,
the bacteria or bacteria mixture in a live state, contained in the treated substance
left after treatment of earth or sand, etc. are completely killed by the heating at
the time of application of the asphalt concrete for road paving. This is because bacteria
or bacteria mixtures are usually killed at approximately 60°C. Further, even in spore
form they are killed at temperatures above 120°C. Accordingly, it is safe to assume
that at temperatures of 160°C and over, bacteria or bacteria mixtures will be completely
killed.
[0103] As a result, it is sanitary to use the foregoing aggregates in asphalt concrete for
road paving, and the biological influence of bacteria or bacteria mixtures on the
asphalt concrete for road paving can be eliminated.
[0104] Next, with respect to use of the recycled sand in cement mortar, the foregoing investigations
yielded the following results.
[0105] Specifically, a recycled sand A, obtained by treating sand with 7% by weight of heavy
oil attached thereto using a nutrient salt culture medium containing the foregoing
heavy oil degrading bacteria nurturing composition and bacteria mixture for 56 days,
and a recycled sand B, obtained by treating sand with 7% by weight of heavy oil attached
thereto using only the nutrient salt culture medium containing the foregoing heavy
oil degrading bacteria nurturing composition, were each dried in a bulk drier and
used as aggregate for cement mortar in the amount of 100% of the total aggregate,
and the performance thereof was confirmed by tests such as a uniaxial compression
test and a flexural test.
[0106] As a result, it was found that the foregoing aggregates were quite satisfactory for
use in a mid-grade cement mortar. Accordingly, it can be expected that the foregoing
aggregates could also be used as a supplementary aggregate in a high-grade cement
mortar.
[0107] With regard to the relationship between the recycled sand A and the recycled sand
B, the cement mortar using the recycled sand A (sand treated with nutritive salt culture
and bacteria mixture) was of slightly better quality.
[0108] The present embodiment explained use of recycled sand obtained by treating sand with
7% by weight of heavy oil attached thereto using a nutrient salt culture medium containing
the foregoing heavy oil degrading bacteria nurturing composition and bacteria mixture,
or using only the nutrient salt culture medium containing the foregoing heavy oil
degrading bacteria nurturing composition, for 56 days, but the present invention is
not necessarily limited to this. It is also possible to use a recycled sand obtained
by treatment for around 21 days, based on Figure 2 (b).
[0109] Further, when using recycled sand obtained by treating sand with 3% by weight of
heavy oil attached thereto using a nutrient salt culture medium containing the foregoing
heavy oil degrading bacteria nurturing composition and bacteria mixture, or using
only the nutrient salt culture medium containing the foregoing heavy oil degrading
bacteria nurturing composition, for 56 days, it goes without saying that the sand
with 3% by weight of heavy oil attached thereto can be treated even more effectively
than the sand with 7% by weight of heavy oil attached thereto.
[0110] Incidentally, the maximum quantity of heavy oil attached to sand is around 10% by
weight of heavy oil; oil in excess of this quantity will be washed away without becoming
attached. Accordingly, investigation of recycled sand obtained by treating sand with
7% by weight of heavy oil attached thereto is sufficient for practical purposes. Further,
oil components are degraded even with sand with 10% by weight of heavy oil attached
thereto, and thus recycled sand obtained thereby can be used as a building and civil
engineering material.
[0111] Further, the present embodiment explained use of a treated substance obtained by
treatment using a nutrient salt culture medium containing the foregoing heavy oil
degrading bacteria nurturing composition and bacteria mixture, or using only the nutrient
salt culture medium containing the foregoing heavy oil degrading bacteria nurturing
composition, but a treated substance obtained by treating earth and sand with heavy
oil attached thereto using at least one of the bacteria strain, bacteria mixture,
and formulation according to the present invention can also be used as an aggregate
or supplementary material in asphalt concrete for road paving or in cement mortar,
i.e., as a building and civil engineering material.
[EXAMPLES]
[0112] Using the preparatory culture medium shown in Table 2 above or the nutrient salt
culture medium shown in Table 5 below as the heavy oil degrading bacteria nurturing
composition according to the present invention, and using crude oil (Arabian light
oil) as the degradation substrate, quantity of oil components degraded was measured
for each of the bacteria TFBOL-1, -2, -3, and -7 according to the present invention,
as follows.
(TABLE 5)
| AMMONIUM NITRATE |
1.0g |
| POTASSIUM PHOSPHATE DIBASIC |
0.1g |
| MAGNESIUM SULFATE HEPTAHYDRATE |
0.2g |
| IRON (III) CHLORIDE HEXAHYDRATE |
0.05g |
| CALCIUM CHLORIDE |
0.02g |
| YEAST EXTRACT |
0.01g |
| SODIUM CHLORIDE |
20.0g |
| DISTILLED WATER |
1000 ml |
| pH |
6.5-7.0 |
(EXAMPLE 1)
[0113] First, TFBOL-1 bacteria were planted in the preparatory culture medium shown in Table
2 above and cultured by shaking (120 strokes/min.; 5cm) at 25°C for four days, yielding
a preparatory culture solution. Next, bacteria were collected from the preparatory
culture solution by centrifuge separation (3500rpm; 20min.), washed twice with a sterilized
preparatory culture medium, and suspended in 1ml of the preparatory culture medium,
yielding lml of a bacteria suspension (bacteria count 10
9/ml).
[0114] To prepare the main culture solution, the foregoing crude oil was added to the nutritive
salt culture medium shown in Table 5 in the amount of 1% by weight, which then underwent
autoclave sterilization at 121°C for 20min. Then 1ml of the foregoing bacteria suspension
was inoculated into 100ml of the main culture solution (in a shaking flask of 500ml
capacity), and was cultured by shaking (120 strokes/min.; 5cm) at 30°C for 10 days.
Bacteria count of the TFBOL-1 bacteria after culturing for 10 days was 6.5×10
9.
[0115] After culturing for 10 days, the main culture solution was subjected to extraction
twice, using 100ml of chloroform per 100ml of culture solution each time. An extract
obtained thereby was sent through a column filled with anhydrous sodium nitrate to
perform dehydration and cell-body elimination, yielding a chloroform extract fraction.
This chloroform extract fraction was dried (60°C; in presence of air flow) until it
reached a constant weight, and this dry weight was treated as a quantity of crude
oil remaining.
[0116] A biodegradation rate was calculated as a quantity of degradation substrate lost
through degradation (%) with respect to the quantity of the degradation substrate
(quantity of crude oil) prior to bacteria inoculation (100%).
[0117] Biodegradation rates were also calculated for each of the bacteria TFBOL-2 through
-8 by the same method as described above. The results are shown in Table 6.
(TABLE 6)
| STRAIN |
BIODEGRADATION RATE (%) |
| TFBOL-1 |
21.1 |
| TFBOL-2 |
28.8 |
| TFBOL-3 |
32.4 |
| TFBOL-4 |
--- |
| TFBOL-5 |
--- |
| TFBOL-6 |
--- |
| TFBOL-7 |
27.6 |
| TFBOL-8 |
--- |
[0118] In Table 6, values are omitted for bacteria strains which, having low degradation
ability for comparatively high-molecule hydrocarbons, showed biodegradation rates
of less than 10%.
[0119] As is evident from Table 6, the bacteria TFBOL-1, TFBOL-2, TFBOL-3, and TFBOL-7 showed
high biodegradation rates of over 10%, indicating that they had high heavy oil degrading
activity.
(EXAMPLE 2)
[0120] Biodegradation rate was measured by performing the same operations as in Example
1 above, except that the bacteria suspension was obtained by suspending 0.5×10
9 each of TFBOL-1, TFBOL-2, TFBOL-3, and TFBOL-7 bacteria in lml of the foregoing preparatory
culture medium. The results are shown in Table 7 below.
(EXAMPLE 3)
[0121] Biodegradation rate was measured by performing the same operations as in Example
1 above, except that the bacteria suspension was obtained by suspending 0.7×10
9 each of the bacteria TFBOL-1 through TFBOL-8 in lml of basic salt culture medium.
The results are shown in Table 7 below.
(TABLE 7)
| STRAIN |
BIODEGRADATION RATE (%) |
| EXAMPLE 2 |
32.3 |
| EXAMPLE 3 |
52.5 |
[0122] As is evident from Table 7, a bacteria mixture including the bacteria TFBOL-1, TFBOL-2,
TFBOL-3, and TFBOL-7, each of which exhibited a high biodegradation rate of over 10%,
showed a biodegradation rate of over 10%, indicating a high heavy oil degrading activity.
Further, a bacteria mixture including all of the bacteria TFBOL-1 through TFBOL-8
showed an even higher biodegradation rate, indicating a high heavy oil degrading activity.
(EXAMPLE 4)
[0123] A chloroform extract fraction using a bacteria mixture according to the present invention
was obtained by performing the same operations as in Example 2 above. Crude oil remaining
in the chloroform extract fraction was separated out by alumina chromatography (activated
alumina: 200 mesh, 60ml, Wako Pure Chemical Industries, Ltd.; glass column: 20×600mm
Pyrex™ glass, flow rate 20ml/h) and classified into saturated hydrocarbons, aromatic
hydrocarbons, asphaltene, and column residue (hereinafter referred to as "Sa," "Ar,"
"As," and "Re," respectively). The Sa fraction obtained in this way was analyzed by
gas chromatography using a predetermined method. Analysis conditions of the gas chromatography
were as follows:
| Column |
Ultra ALLOY Capillary Column DX30 (15m, 0.5m) |
| Oven temp. |
100°C (0min) to 250°C (30min), 4°C/min |
| Injector temp. |
250°C |
| Detection temp. |
250°C |
| Detector |
FID |
| Carrier gas |
helium |
[0124] Figures 1(a) and 1(b) are explanatory drawings showing elution patterns for Sa fractions
of equal quantity before and after treatment, using a common scale intensity on the
vertical axis. As shown in Figures 1(a) and 1(b), using a bacteria mixture according
to the present invention can degrade all saturated hydrocarbons having less than 35
carbon atoms, which are crude oil components.
(EXAMPLE 5)
[0125] 1kg of sand containing 3% by weight of heavy oil C as the heavy oil was mixed with
100ml of a nutritive salt culture medium having the composition shown in Table 5 above
as a heavy oil decomposing bacteria nurturing composition according to the present
invention, and with 1×10
9 each of the bacteria TFBOL-1 through TFBOL-8 as a bacteria mixture according to the
present invention. After mixing, the sand was placed in a bag and buried at the seashore,
and every seven days a predetermined quantity of the sand was sampled and a remaining
oil quantity (quantity of oil remaining) was measured using the same method of measuring
remaining crude oil quantity as in Example 1 above. Considering the quantity of oil
in the sand containing 3% by weight of heavy oil on the first day (prior to treatment)
as 100%, change over time of the quantity of oil remaining was investigated by calculating
a quantity of oil remaining (%) once every seven days. The results are shown in Figure
2(a). Further, an Sa fraction was obtained for the sand sampled on the 7th and 56th
days by performing the same operations as in Example 4 above, which was then analyzed
by gas chromatography. The results are shown in Figures 3(a) through 3(c). Figures
3(a) through 3(c), and Figures 4(a) through 4(c) to be discussed below, like Figures
1(a) and 1(b) above, are explanatory drawings which use a common scale intensity on
the vertical axis. Further, as a control, change over time of an equal quantity of
untreated sand was also investigated. The results for the control are also shown in
Figure 2(a).
(EXAMPLE 6)
[0126] Sand containing 3% by weight of heavy oil was treated using the same method as in
Example 5 above, except that the foregoing bacteria mixture was not added, and change
over time in quantity of oil remaining was investigated and an Sa fraction was analyzed
by gas chromatography. The results are shown in Figure 2(a) and in Figures 4(a) through
4(c).
(EXAMPLES 7 AND 8)
[0127] Using the same methods as in Examples 5 and 6 above, sand containing 7% by weight
of heavy oil was treated, and change over time in quantity of oil remaining was investigated.
The results are shown in Figure 2(b). An Sa fraction was also analyzed by gas chromatography.
[0128] As shown in Figure 2 (a) , at a point 14 days after commencing the experiment, the
quantity of oil remaining in the untreated sand containing 3% by weight of heavy oil
(the control) had decreased by only 3.1%. In contrast, in the sand treated using only
the nutritive salt culture medium containing the heavy oil degrading bacteria nurturing
composition (Example 6), quantity of oil remaining was decreased by 34%, and in the
sand treated using both the nutritive salt culture medium containing the heavy oil
degrading bacteria nurturing composition and the bacteria mixture (Example 5), there
was a sharp decrease of 44% in quantity of oil remaining.
[0129] Further, as shown in Figure 2(b), at a point 21 days after commencing the experiment,
the quantity of oil remaining in the untreated sand containing 7% by weight of heavy
oil (the control) had decreased by only 2.3%. In contrast, in the sand treated using
only the nutritive salt culture medium containing the heavy oil degrading bacteria
nurturing composition (Example 8), quantity of oil remaining was decreased by 28%,
and in the sand treated using both the nutritive salt culture medium containing the
heavy oil degrading bacteria nurturing composition and the bacteria mixture (Example
7), there was a sharp decrease of 46.7% in quantity of oil remaining.
[0130] As the foregoing results show, rate of heavy oil degradation was fastest with treatment
using both the nutritive salt culture medium containing the heavy oil degrading bacteria
nurturing composition and the bacteria mixture, and treatment using only the nutritive
salt culture medium containing the heavy oil degrading bacteria nurturing composition
showed the next fastest rate of heavy oil degradation. From this it is evident that
with treatment using both the nutritive salt culture medium containing the heavy oil
degrading bacteria nurturing composition and the bacteria mixture, heavy oil degradation
proceeded at a high rate due to the bacteria mixture, and with treatment using only
the nutritive salt culture medium containing the heavy oil degrading bacteria nurturing
composition, heavy oil degradation proceeded at a high rate due to the growth and
activity of hydrocarbon degrading bacteria ordinarily present on seashores, promoted
by the heavy oil degrading bacteria nurturing composition.
[0131] Incidentally, in the heavy oil C used in the foregoing experiment, quantities of
saturated hydrocarbons and aromatic hydrocarbons of low boiling point which dissolve
in water or evaporate are so small as to be insignificant. For this reason, the quantity
of loss of such saturated hydrocarbons and aromatic hydrocarbons of low boiling point
can be disregarded.
[0132] Further, as shown in Figures 3(a) through 3(c) and 4(a) through 4(c), treatment using
both the nutritive salt culture medium containing the heavy oil degrading bacteria
nurturing composition and the bacteria mixture, or treatment using only the nutritive
salt culture medium containing the heavy oil degrading bacteria nurturing composition,
degraded all saturated hydrocarbons having less than 35 carbon atoms, which are crude
oil components, and this degradation was especially rapid with treatment using both
the nutritive salt culture medium containing the heavy oil degrading bacteria nurturing
composition and the bacteria mixture.
(EXAMPLE 9)
[0133] 1kg of sand containing 3% by weight of heavy oil C as the heavy oil was mixed with
100ml of a nutritive salt culture medium having the composition shown in Table 5 above,
which contains a heavy oil decomposing bacteria nurturing composition, and with 1×10
9 each of the TFBOL-1, -2, -3, and -7 bacteria as a bacteria mixture according to the
present invention. After mixing, the sand was placed in a bag and buried at the seashore,
and a predetermined quantity of the sand was sampled on the first day (prior to treatment)
and after 14 days.
[0134] The sampled sand was classified into Sa, Ar, As, and Re fractions in the same manner
as in Example 4 above, and each fraction obtained in this way was analyzed by gas
chromatography in order to measure change in the heavy oil components in the sand
containing 3% by weight of heavy oil. Analysis conditions of the gas chromatography
were as follows:
| Column |
Ultra ALLOY Capillary Column DX30 (15m, 0.5m) |
| Oven temp. |
100°C (Omin) to 250°C (30min), 4°C/min |
| Injector temp. |
250°C |
| Detection temp. |
250°C |
| Detector |
FID |
| Carrier gas |
helium |
(EXAMPLE 10)
[0135] Sand containing 3% by weight of heavy oil was treated using the same method as in
Example 9 above, except that the foregoing bacteria mixture was not added, in order
to measure change in the heavy oil components in the sand due to action of the nutritive
salt culture medium containing the heavy oil degrading bacteria nurturing composition
according to the present invention.
[0136] As shown in Figure 5(a), at a point 14 days after commencing the experiment, use
of the bacteria mixture according to the present invention (Example 9) had greatly
degraded the Sa fraction. Further, treatment using only the nutritive salt culture
medium containing the heavy oil degrading bacteria nurturing composition according
to the present invention (Example 10) showed the second greatest degradation of the
Sa fraction after treatment using the bacteria mixture.
(EXAMPLE 11)
[0137] Using the same method as in Example 9 above, sand containing 7% by weight of heavy
oil was treated, and change in the heavy oil components was measured after 21 days.
The results are shown in Figure 5(b).
(EXAMPLE 12)
[0138] Sand containing 7% by weight of heavy oil was treated using the same method as in
Example 11 above, except that the foregoing bacteria mixture was not added, in order
to measure change in the heavy oil components in the sand due to action of the heavy
oil degrading bacteria nurturing composition according to the present invention.
[0139] As shown in Figures 5(a) and 5(b), at a point 14 days or 21 days after commencing
the experiment, use of the bacteria mixture according to the present invention (Examples
9 and 11) had greatly degraded the Sa fraction. Further, treatment using only the
nutritive salt culture medium containing the heavy oil degrading bacteria nurturing
composition according to the present invention (Examples 10 and 12) showed the second
greatest degradation of the Sa fraction after treatment using the bacteria mixture.
(EXAMPLE 13)
[0140] The present embodiment will discuss the results of an investigation of whether sand
(hereinafter referred to as "recycled sand") obtained by treating sand with heavy
oil attached thereto using a nutritive salt culture medium containing the foregoing
heavy oil degrading bacteria nurturing composition and a bacteria mixture, or using
only the nutritive salt culture medium containing the foregoing heavy oil degrading
bacteria nurturing composition can be used in asphalt concrete for road paving.
[0141] This investigation was carried out by performing an experiment regarding whether
asphalt concrete containing the recycled sand as a supplementary aggregate meets the
standards for asphalt concrete for road paving.
[0142] Two kinds of recycled sand were used: recycled sand A, obtained by treating sand
with 7% by weight of heavy oil attached thereto using a nutrient salt culture medium
containing the foregoing heavy oil degrading bacteria nurturing composition and a
bacteria mixture for 56 days, and a recycled sand B, obtained by treating sand with
7% by weight of heavy oil attached thereto using only the nutrient salt culture medium
containing the foregoing heavy oil degrading bacteria nurturing composition.
[0143] The aggregate blending conditions were as shown in Table 8 below. Specifically, in
blend 1, recycled sand A made up 15% of the total aggregate, and in blend 2, recycled
sand B made up 15% of the total aggregate. Further, blend 3 shows typical blending
conditions in conventional asphalt concrete for road paving, in which neither recycled
sand A nor recycled sand B is used. Here, recycled sands A and B were dried in a bulk
drier at 11°C for 24 hours, and heated at 180°C for 16 hours.
(TABLE 8)
| AGGREGATE MATERIAL |
BLEND 1 (%) |
BLEND 2 (%) |
BLEND 3 (%) |
| NO. 6 CRUSHED ROCK |
38 |
38 |
38 |
| NO. 7 CRUSHED ROCK |
15 |
15 |
15 |
| SCREENINGS (SC) |
13 |
13 |
17 |
| COARSE SAND |
5 |
5 |
5 |
| FINE SAND |
9 |
9 |
13 |
| RECYCLED SAND A |
15 |
--- |
--- |
| RECYCLED SAND B |
--- |
15 |
--- |
| ROCK POWDER |
5 |
5 |
5 |
[0144] Next, Table 9 shows the respective particle sizes of each of the aggregate materials
listed above prior to blending.
(TABLE 9)
| SCREEN SIZE (mm) |
CRUSHED ROCK (%) |
SC (%) |
SAND (%) |
RECYCLED SAND (%) |
ROCK POWDER (%) |
| |
NO.6 |
NO.7 |
|
COARSE |
FINE |
A |
B |
|
| 19 |
100.0 |
|
|
|
|
|
|
|
| 13.2 |
91.5 |
100.0 |
|
100.0 |
100.0 |
100.0 |
100.0 |
|
| 4.75 |
1.4 |
93.6 |
100.0 |
98.3 |
99.8 |
99.7 |
99.9 |
|
| 2.36 |
0.7 |
13.6 |
83.8 |
91.2 |
99.0 |
49.9 |
54.4 |
|
| 0.6 |
0.6 |
1.1 |
36.4 |
60.2 |
92.0 |
22.5 |
24.3 |
100.0 |
| 0.3 |
|
0.8 |
23.9 |
20.0 |
62.4 |
17.6 |
20.0 |
97.0 |
| 0.15 |
|
|
16.0 |
3.3 |
2.4 |
3.2 |
2.5 |
92.0 |
| 0.075 |
|
|
9.4 |
1.5 |
0.7 |
0.3 |
0.2 |
72.0 |
[0145] Further, Table 10 shows the respective particle size distributions for each of the
blends 1, 2, and 3 compounded of the aggregate materials having the respective particle
sizes shown in Table 9 above. Each of these satisfies the general specifications for
asphalt concrete for road paving set forth in the right-most column of Table 10.
(TABLE 10)
| SCREEN SIZE (mm) |
BLEND 1 (%) |
BLEND 2 (%) |
BLEND 3 (%) |
STANDARD PARTICLE SIZE RANGE (%) |
| 19 |
100 |
100 |
100 |
100 |
| 13.2 |
96.8 |
96.8 |
96.8 |
95-100 |
| 4.75 |
61.4 |
61.4 |
61.0 |
55-70 |
| 2.36 |
39.2 |
39.9 |
40.0 |
35-50 |
| 0.6 |
24.8 |
25.0 |
26.6 |
18-30 |
| 0.3 |
17.3 |
17.7 |
18.3 |
10-21 |
| 0.15 |
7.5 |
7.4 |
7.7 |
6-16 |
| 0.075 |
5.0 |
5.0 |
5.4 |
4-8 |
[0146] Next, Table 11 shows mixing conditions and compaction conditions for asphalt concrete
for road paving. Here, the asphalt used was "straight asphalt 60 to 80" defined in
JIS K 2207 "Petroleum Asphalt." Straight asphalt 60 to 80 has a needle penetration
at 25°C of more than 40 but no more than 60.
(TABLE 11)
| ITEM |
CONDITIONS |
| ASPHALT QUANTITY |
5.8% |
| AGGREGATE HEATING TEMPERATURE |
TARGET 160°C - 170°C |
| ASPHALT HEATING TEMPERATURE |
TARGET 150°C - 160°C |
| MIXING TEMPERATURE |
TARGET 152°C - 157°C |
| COMPACTION TEMPERATURE |
TARGET 140°C - 145°C |
| NUMBER OF COMPACTIONS |
50 TIMES EACH ON FRONT AND BACK |
[0147] Tests performed, in addition to apparent density, were a flow test, a Marshall stability
test, and a residual stability test, as stipulated in the general specifications for
asphalt concrete for road paving. Conditions for the Marshall stability test and the
residual stability test were as shown in Table 12 below.
(TABLE 12)
| ITEM |
CONDITIONS |
| MARSHALL STABILITY TEST (AS PER ASPHALT PAVING SPECIFICATIONS) |
CURING TEMP.: 60°C |
| CURING TIME: 30 MINUTES |
| RESIDUAL STABILITY TEST (AS PER ASPHALT PAVING SPECIFICATIONS) |
CURING TEMP.: 60°C |
| CURING TIME: 48 HOURS |
[0148] The results of tests performed under the foregoing conditions are shown in Table
13 below.
(TABLE 13)
| ITEM |
BLEND 1 |
BLEND 2 |
BLEND 3 |
STANDARD VALUES |
| APPARENT DENSITY (g/cm3) |
2.373 |
2.378 |
2.364 |
--- |
| FLOW VALUE (1/100cm) |
29.3 |
23.0 |
24.7 |
20-40 |
| STABILITY (Kg) |
1031.7 |
1008.3 |
935.0 |
≥ 500 |
| RESIDUAL STABILITY (%) |
93.7 |
94.4 |
98.2 |
≥ 75 |
| VISUAL OBSERVATION DURING TEST |
SOME ASPHALT SEEPAGE DURING PREPARATION OF SPECIMEN |
--- |
--- |
[0149] The results in Table 13 show that both blend 1, which used recycled sand A, and blend
2, which used recycled sand B, satisfy standard values for quality of asphalt concrete
for road paving.
[0150] In other words, it was found that both an aggregate containing as supplementary aggregate
15% of the recycled sand A, obtained by treating sand with 7% by weight of heavy oil
attached thereto using a nutritive salt culture medium containing the heavy oil degrading
bacteria nurturing composition according to the present invention and a bacteria mixture
for 56 days, and an aggregate containing as supplementary aggregate 15% of the recycled
sand B, obtained by treating sand with 7% by weight of heavy oil attached thereto
using only the nutritive salt culture medium containing the heavy oil degrading bacteria
nurturing composition according to the present invention for 56 days, can be used
in asphalt concrete for road paving.
(EXAMPLE 14)
[0151] The present embodiment will discuss the results of an investigation of whether recycled
sand obtained by treating sand with heavy oil attached thereto using the foregoing
bacteria or bacteria mixture can be used in cement mortar.
[0152] This investigation used the two kinds of recycled sand used in Example 13 above,
i.e. the recycled sand A, obtained by treating sand with 7% by weight of heavy oil
attached thereto using a nutritive salt culture medium containing the heavy oil degrading
bacteria nurturing composition according to the present invention and a bacteria mixture
for 56 days, and the recycled sand B, obtained by treating sand with 7% by weight
of heavy oil attached thereto using only the nutritive salt culture medium containing
the heavy oil degrading bacteria nurturing composition according to the present invention
for 56 days. In order to apply the recycled sand A and the recycled sand B to cement
mortar, each type of recycled sand was mixed with cement as an aggregate to prepare
a specimen for strength tests, and then uniaxial compression strength and flexural
strength of this specimen were measured. These tests were carried out as stipulated
in JIS R 5201 "Methods of Performing Physical Testing of Cement."
[0153] Particle size distributions of the recycled sand A and the recycled sand B were as
shown in Table 14 below.
(TABLE 14)
| SCREEN SIZE (mm) |
RECYCLED SAND A (%) |
RECYCLED SAND B (%) |
| 13.2 |
100.0 |
100.0 |
| 4.75 |
99.7 |
99.9 |
| 2.36 |
49.9 |
54.4 |
| 0.6 |
22.5 |
24.3 |
| 0.3 |
17.6 |
20.0 |
| 0.15 |
3.2 |
2.5 |
| 0.075 |
0.3 |
0.2 |
[0154] With regard to the method of performing the strength tests, a form for preparing
the specimen was made up of three forms of 4×4×16cm each, connected together. The
specimen was obtained by mixing ordinary Portland cement with aggregate and water
at an aggregate/cement ratio (S/C) of 2 and a water/cement ratio (W/S) of 65%. Prior
to pouring the mixed cement mortar into the form, a flow test was performed.
[0155] The specimen was prepared using the above form, and removed from the form the next
day. After weighing the specimen, water curing was commenced by placing the specimen
in a water bath at 20°C ± 3°C. The specimen was taken out of the bath after seven
days and after 28 days, at which time it was weighed, and a uniaxial compression test
and a flexural test were performed thereon.
[0156] Table 15 shows the results of the flow tests, and Table 16 the results of the strength
tests. In the flow tests, a flow cone was filled with mixed cement and raised upwards.
The flow values shown in Table 15 are abstract numbers expressing in mm the diameter
of mortar spreading out from the base of the flow cone at this time.
(TABLE 15)
| FLOW VALUE |
RECYCLED SAND A + CEMENT + WATER (S/C=2; W/C=65%) |
RECYCLED SAND B + CEMENT + WATER (S/C=2; W/C=65%) |
| MAXIMAL VALUE |
221.8 |
235.4 |
| MINIMAL VALUE |
211.7 |
234.7 |

[0157] Standards stipulated by JIS for high-grade cement mortar specify compression strength
values of not less than 14.71N/mm
2 at a material age of seven days, and not less than 29.42N/mm
2 at a material age of 28 days. Typical measured values for compression strength are
around 25N/mm
2 at a material age of seven days, and around 41N/mm
2 at a material age of 28 days. Further, typical measured values for flexural strength
are around 5N/mm
2 at a material age of seven days, and around 7N/mm
2 at a material age of 28 days.
[0158] In light of these values, the results in Table 16 above show that both cement mortar
containing blend 1, which used recycled sand A, and cement mortar containing blend
1, which used recycled sand B, satisfied the standard of a compression strength value
of not less than 14.71N/mm
2 at seven days. However, at 28 days, both showed compression strength values slightly
less than the standard of 29.42N/mm
2.
[0159] With regard to flexural strength, both of the above cement mortars showed flexural
strength values slightly less than the typical values for flexural strength of around
5N/mm
2 at seven days and around 7N/mm
2 at 28 days.
[0160] With regard to the relationship between the recycled sand A and the recycled sand
B, the cement mortar using the recycled sand A showed slightly better strength.
[0161] The foregoing results indicate that a cement mortar in which the aggregate is entirely
made up of the recycled sand A or the recycled sand B is fully adequate, not as a
high-grade cement mortar, but as a mid-grade cement mortar.
[0162] Incidentally, the foregoing test results were obtained using aggregates entirely
made up of the recycled sand A or the recycled sand B; a cement mortar using recycled
sand as a supplementary aggregate, as in the asphalt concrete for road paving in Example
13, can be expected to be fully satisfactory for use as a high-grade cement mortar.
[0163] As discussed above, the novel strain of bacteria according to the present invention
having a heavy oil degrading ability may be FERMBP-7046, a strain belonging to the
genus Acinetobacter.
[0164] Further, as discussed above, the novel strain of bacteria according to the present
invention having a heavy oil degrading ability may be FERMBP-7049, a strain belonging
to the genus Acinetobacter.
[0165] Further, as discussed above, the novel strain of bacteria according to the present
invention having a heavy oil degrading ability may be FERMBP-7047, a strain belonging
to the genus Pseudomonas.
[0166] Further, as discussed above, the novel strain of bacteria according to the present
invention having a heavy oil degrading ability may be FERMBP-7048, a strain belonging
to the genus Alcaligenes.
[0167] As discussed above, a bacteria mixture according to the present invention may include
at least one kind of bacteria having a heavy oil degrading ability selected from the
group consisting of: FERMBP-7046, a strain of Acinetobacter; FERMBP-7049, a strain
of Acinetobacter; FERMBP-7047, a strain of Pseudomonas; and FERMBP-7048, a strain
of Alcaligenes.
[0168] The foregoing bacteria or bacteria mixture was discovered when bacteria were isolated
from seawater in order to discover a strain having a hydrocarbon degrading ability
in nutrient-poor conditions as close as possible to those in the natural world. Thus,
the above bacteria or bacteria mixture can be readily grown on inexpensive nutrition
sources and degrade hydrocarbon efficiently. Accordingly, leaked oil components, for
example, can be easily and efficiently removed through degradation at a low cost by
using the foregoing bacteria or bacteria mixture.
[0169] As discussed above, a heavy oil degrading bacteria nurturing composition of the present
invention may include 40 to 90 wt% of ammonium nitrate, 1 to 50 wt% of potassium phosphate
dibasic, 2 to 50 wt% of magnesium sulfate, 1 to 20 wt% of iron (III) chloride, 0.2
to 15 wt% of calcium chloride, and 0.1 to 10 wt% of yeast extract as effective components.
[0170] With this structure, the heavy oil degrading bacteria nurturing composition can be
prepared inexpensively, and can promote growth of heavy oil degrading bacteria and
the activation of heavy oil degradation. Consequently, leaked oil components, for
example, can be removed through degradation inexpensively, simply, and effectively
by causing the heavy oil degrading bacteria nurturing composition to act on the oil
components by e.g. scattering the heavy oil degrading bacteria nurturing composition
alone, or in an aqueous solution prepared by dissolving it in 500 to 2000 times its
weight of e.g. seawater, or with the addition of the foregoing bacteria mixture.
[0171] As discussed above, the formulation according to the present invention may include
the foregoing heavy oil degrading bacteria nurturing composition.
[0172] Further, as discussed above, the formulation according to the present invention may
include one or more of the foregoing heavy oil degrading bacteria or the foregoing
bacteria mixture and the heavy oil degrading bacteria nurturing composition set forth
in claim 6 hereinbelow.
[0173] With this structure, oil components in an object of treatment such as sand can be
degraded by simple operations such as scattering the object of treatment with the
present formulation, prepared, for example, by dissolving the foregoing bacteria or
bacteria mixture, the foregoing heavy oil degrading bacteria nurturing composition,
etc. in an aqueous solution, or forming the same into pellets, or impregnating the
same into an organic material in sheet form.
[0174] As discussed above, a method of treating oil components according to the present
invention uses at least one of: one or more of the foregoing oil degrading bacteria,
the foregoing bacteria mixture, the foregoing heavy oil bacteria nurturing composition,
and the foregoing formulation.
[0175] With this method, the above bacteria or bacteria mixture can be readily grown on
inexpensive nutrition sources and degrade hydrocarbon efficiently. Accordingly, leaked
oil components, for example, can be easily and efficiently removed through degradation
at a low cost.
[0176] As discussed above, a building and civil engineering material according to the present
invention may contain a treated substance obtained by treating earth and sand with
heavy oil attached thereto using at least one of: one or more of the foregoing oil
degrading bacteria, the foregoing bacteria mixture, the foregoing heavy oil bacteria
nurturing composition, and the foregoing formulation.
[0177] With this structure, in a treated substance obtained by treating earth and sand with
heavy oil attached thereto using at least one of the bacteria, bacteria mixture, heavy
oil degrading bacteria nurturing composition, and formulation according to the present
invention, the heavy oil has been degraded, leaving recycled sand. Further, this recycled
sand is suitable for use as a building and civil engineering material.
[0178] Consequently, by using at least one of the foregoing bacteria, bacteria mixture,
heavy oil degrading bacteria nurturing composition, and formulation to treat earth
and sand containing heavy oil washed ashore from e.g. a tanker which has run aground,
a treated substance (recycled sand) can be obtained which is suitable for use as a
building and civil engineering material, i.e., in asphalt concrete for road paving
or in cement mortar.
[0179] As a result, earth and sand with heavy oil attached thereto, which conventionally
were incinerated and buried, for example, can be recycled and provided for use as
a building and civil engineering material.
[0180] The embodiments and Examples discussed in the foregoing detailed explanation serve
solely to illustrate the technical details of the present invention, which should
not be narrowly interpreted within the limits of such embodiments and concrete examples,
but rather may be applied in many variations, provided such variations do not depart
from the spirit of the present invention or exceed the scope of the patent claims
set forth below.
[0181] A bacteria strain FERMBP-7046 belonging to the genus Acinetobacter, a strain FERMBP-7049
belonging to the genus Acinetobacter, a strain FERMBP-7047 belonging to the genus
Pseudomonas, and a strain FERMBP-7048 belonging to the genus Alcaligenes are caused
to act on an object of treatment, either individually or in a bacteria mixture including
at least one of the foregoing strains. Thus it is possible to provide heavy oil degrading
bacteria and a heavy oil degrading bacteria mixture which are inexpensively prepared,
which simplify degradation and removal operations, and which can be stored and shipped
simply, and to provide a nurturing composition for such bacteria, a method of degrading
heavy oil using such bacteria, and building and civil engineering materials containing
a substance obtained by heavy oil degradation treatment.